Siloxane removal via silicate formation for lifetime extension of photocatalytic devices

ABSTRACT

A photocatalytic device for reacting with volatile organic compounds includes a photocatalyst and at least one additive, such as hafnium oxide and zirconium oxide, that is capable of forming a stable silicate with silicon dioxide. The additive reacts with volatile silicon-containing compounds to form stable silicate compounds. As a result, the silicon-containing compounds are unavailable for deactivation of the photocatalyst.

CROSS-REFERENCE TO RELATED APPLICATION(S)

This is a continuation of International Application PCT/US2007/017113, with an international filing date of Jul. 31, 2007.

BACKGROUND

This invention relates generally to use of ultraviolet photocatalytic oxidation (UV-PCO) technology for improved decontamination of fluid in fluid purifier systems, especially in air purifier systems. More specifically, the present invention relates to a device for reducing the deactivation of photocatalytically active oxides used in UV-PCO technology by volatile silicon-containing compounds.

Some buildings utilize air purification systems to remove airborne substances such as benzene, formaldehyde, and other contaminants from the air supply. Some of these purification systems include photocatalytic reactors that utilize a substrate or cartridge containing a photocatalyst oxide. When placed under an appropriate light source, typically a UV light source, the photocatalyst oxide interacts with airborne water molecules to form hydroxyl radicals. The hydroxyl radicals then attack the contaminants and initiate an oxidation reaction that converts the contaminants into less harmful compounds, such as water and carbon dioxide. It is further believed that the combination of water vapor, suitably energetic photons and a photocatalyst also generates an active oxygen agent like hydrogen peroxide (W. Kubo and T. Tatsuma, Analytical Sciences 20 2004 591-593).

A commonly used UV photocatalyst is titanium dioxide (TiO₂), otherwise referred to as titania. Degussa P25 titania and tungsten oxide grafted titania catalysts (such as tungsten oxide on P25) have been found to be especially effective at removing organic contaminants under UV light sources.

A problem with air purification systems using UV-PCO technology has arisen. Currently available systems exhibit a significant loss in catalytic ability over time. This loss of catalytic ability has been attributed to volatile silicon-containing compounds (VSCCs), such as certain siloxanes, in the air.

The aggregate amount of volatile organic compounds (VOCs) in air is typically on the order of 1 part per million by volume. In contrast, VSCC concentrations are two or more orders of magnitude lower. These VSCCs arise primarily from the use of certain personal care products, such as deodorants, shampoos, and the like, or dry cleaning fluids. They can also arise from the use of RTV silicone caulks, adhesives and the like. When these VSCCs are oxidized on the photocatalyst of a UV-PCO system, they form relatively non-volatile compounds containing silicon and oxygen that may deactivate the photocatalyst. Examples of non-volatile compounds of silicon and oxygen include silicon dioxide, silicon oxide hydride, silicon hydroxide, high order polysiloxanes and the like. These compounds may be at least partially hydrated when water vapor is present. Increasing the catalyst surface area does not necessarily slow the rate of deactivation as might be expected if the deactivation occurred by direct physical blockage of the active sites by the resultant non-volatile compound containing silicon and oxygen.

There is a need for improved UV-PCO systems that can aid in the elimination of fluid borne contaminants in a fluid purifier and can operate effectively in the presence of typically encountered levels of volatile silicon-containing compounds such as siloxanes.

SUMMARY

A photocatalytic device includes photocatalyst in conjunction with an additive that protects the photocatalyst from deactivation caused by volatile silicon-containing compounds. The additive includes particles or crystals of one or more compounds capable of forming a stable silicate or solid solution with inorganic compounds containing silicon and oxygen, such as silicon dioxide. The additive, which may be interspersed with the photocatalyst or may be in the form of islands or an incomplete overlayer on a photocatalyst layer or a photocatalyst particle, reacts with volatile or semivolatile silicon-containing compounds or their oxidation product(s) to form a stable silicate or solid solution. The additive sequesters the silicon-containing contaminants from the photocatalyst, so that they are not available to react with and deactivate the photocatalyst. Examples of additives include hafnia (HfO₂), zirconia (ZrO₂), niobia (Nb₂O₅), alumina (Al₂O₃), magnesia (MgO), yttria (Y₂O₃), tantala (Ta₂O₅), ytterbia (Yb₂O₃), chromia (Cr₂O₃), scandia (Sc₂O₃), other rare earth oxides and mixtures and combinations of these compounds, for example yttrium stabilized zirconia and hafnia.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 schematically illustrates a photocatalytic air purification device.

FIG. 2 is a phase diagram of the ZrO₂/SiO₂ system.

FIG. 3 is a phase diagram of the HfO₂/SiO₂ system.

DETAILED DESCRIPTION

FIG. 1 is a schematic diagram of air purifier system 10, which uses ultraviolet photocatalytic oxidation (UV-PCO) to remove contaminants from air. Air purifier system 10 includes inlet 12, outlet 14, photocatalytic reactor 18 (which includes substrate 20, photocatalytic coating 22, UV source 24), fan 26 and heater 28. An optional collector 30 may be used to temporarily collect certain volatile compounds such as VOCs prior to transfer through the photocatalytic reactor 18. For example, an adsorbent bed (e.g. activated carbon, zeolites, etc.) may be used to collect VOCs for subsequent release (e.g. through heating and subsequent volatilization of the collected VOCs) into the photocatalytic reactor 18. Collector 30 may be integrated or incorporated into prefilter 16.

Ambient air is drawn into the system 10 through inlet 12 by fan 26. Airstream A passes through prefilter 16, and then through photocatalyst reactor 18 and fan 26 to outlet 14. Prefilter 16 removes dust and particles by trapping the dust and particles. Within photocatalyst reactor 18, ultraviolet radiation from UV source 24 is absorbed by photocatalyst coating 22, which causes photocatalyst coating 22 to interact with airborne water molecules to produce reactive species such as hydroxyl radicals, hydrogen peroxide, hydrogen peroxide radicals, and superoxide ions. These reactive species interact with VOCs in the air to transform the VOCs into byproducts such as carbon dioxide and water. Therefore, airstream A contains less contaminants as it exits system 10 through outlet 14 than it contained when it entered system 10 through inlet 12.

In FIG. 1 substrate 20 is illustrated schematically as a flat plate. In practice, substrate 20 can take a number of different forms, which may be configured to maximize the surface area on which photocatalytic coating 22 is located or to maximize the extent of nonlaminar flow through the substrate. One example is a honeycomb structure on which photocatalytic coating 22 is deposited and through which airstream A passes. Another example is a segmented and radially offset array of discrete honeycomb structures on which photocatalytic coating 22 is deposited and through which airstream A passes.

Experimental evidence has highlighted the need to protect the photocatalyst coating 12 from contamination and deactivation by volatile silicon-containing compounds. The major source of these VSCCs is believed to be the family of compounds containing volatile methyl siloxanes (VMS) commonly found in cleaners, personal deodorants, shampoos, and a variety of other personal and commercial products. Common members of the VMS family include hexamethyl cyclotrisiloxane and octamethyl cyclotetrasiloxane, often referred to D₃ and D₄, respectively. Larger molecules D₅, D₆, D₇ and so on are also known. Related volatile silicon-containing compounds, including linear siloxanes, are also of concern.

It is most desirable to remove VSCCs from the incoming air stream upstream of photocatalytic reactor 18, but it is also important to protect photocatalytic reactor 18 from any VSCCs in the air stream that reach photocatalytic reactor 18 and come in contact with photocatalyst coating 22.

In the present invention, additives intermixed with the photocatalyst within photocatalyst coating 22, or deposited on the surface of photocatalyst coating 22 in the form of islands or an incomplete layer act as sequestering agents to prevent VSCCs from reaching the photocatalyst and contaminating or deactivating it. The additives include one or more compounds that are capable of reacting with VSCCs to form a stable silicate(s) or solid solution(s) with inorganic compounds containing silicon and oxygen, such as silicon dioxide. As a result, the additives permanently remove the VSCCs from the air stream and prevent them from contacting and deactivating the photocatalyst.

Examples of additives capable of forming a stable silicate with silicon dioxide include hafnia (HfO₂), zirconia (ZrO₂), alumina (Al₂O₃), magnesia (MgO), yttria (Y₂O₃), tantala (Ta₂O₅), ytterbia (Yb₂O₃), chromia (Cr₂O₃), scandia (Sc₂O₃), other rare earth oxides and mixtures of these compounds. Specific oxide systems containing HfO₂ and ZrO₂ will form stable silicates with SiO₂, for example HfSiO₄ and ZrSiO₄, respectively. These silicate compounds are stable line compounds in the phase diagrams of these binary systems, and therefore will lock up the silicon-containing species and render them unavailable for deactivation of the nearby TiO₂ based photocatalyst. MgO forms a stable line compound MgSiO₃ with SiO₂. Other oxides form stable silicates with SiO₂ without forming line compounds (e.g. solid solutions, Nb₂O₅, Ta₂O₅ and Cr₂O₃). Other oxides form stable silicates with SiO₂ yet form more than one line compound with SiO₂ (e.g. Y₂O₃, Yb₂O₃, and Sc₂O₃). Titanium dioxide (TiO₂) does not form a similarly stable line compound with SiO₂.

Phase diagrams for the zirconia and hafnia systems are shown in FIGS. 2 and 3, respectively. In both cases, the stable line silicate forms at an equal molar ratio (1:1) of the end member oxides (for example ZrO₂/SiO₂ and HfO₂/SiO₂). The phase diagrams show that a stable silicate will be present in all compositions containing SiO₂. Free silica (as quartz) will only be present above a 50 mol percent level of silica. Thermodynamic data for the reaction of ZrO₂+SiO₂=ZrSiO₄ indicates the reaction is favorable (ΔG<0) for the temperature range of 0° C. to about 1700° C. An analogous reaction based on HfO₂ can be expected to behave similarly.

A photocatalyst coating with an additive capable of forming a stable silicate can be produced in a variety of different ways. Some examples are as follows:

First, a photocatalyst layer having interspersed additive particles can be formed by separately producing photocatalyst particles and additive particles. The additive, such as ZrO₂, HfO₂, mixed ZrO₂/HfO₂, yttria or magnesia stabilized zirconia, rare earth modified ZrO₂ or HfO₂ or other suitable oxides or mixture of oxides can be added as a particulate filler in a slurry containing the photocatalyst prior to coating deposition. The slurry is typically an aqueous slurry that is coated onto the substrate and then dried to produce the photocatalyst coating. The additive particles are dispersed within the coating, and provide sites at which volatile silicon-containing compounds can react to form a stable silicate. Additive particles can be uniformly sized or bi- or multimodally distributed and may be sized similarly to or different than the photocatalytic particles. Dispersants, pH modifiers, surfactants and the like may be used to adjust the properties of the slurry to render it suitable for processing.

Second, a mixture of the photocatalyst and the additives can be created with a sol-gel or co-precipitation method by the use of appropriate precursors. An example of a process for forming a photocatalyst using a sol-gel process is described in PCT application PCT/US07/12882 entitled “Deactivation Resistant Photocatalyst and Method of Preparation” filed May 31, 2007, which is incorporated by reference.

A sol-gel process for forming photocatalyst coatings with intermixed additives can follow the same general steps described in the above-mentioned PCT application. Template creation begins with the addition of a first precursor to a solution to produce a first controlled hydrolysis reaction. The first precursor includes, for example, a zirconium-containing precursor or hafnium-containing precursor, or both, or another oxide precursor or mixture of precursors selected to provide the appropriate metal species. The solution may include one or more low molecular weight polymer components, and one or more salts.

After the first hydrolysis reaction is complete, a second precursor is added to the solution in order to form the photocatalyst. The second precursor, may be, for example, a titanium-containing precursor. One or more metal salts may also be added to the solution to ultimately form a wide band gap metal oxide semiconductor in addition to titanium dioxide. Examples of metal salts include salts of tin, iron, neodymium, zinc and cerium.

After the second hydrolysis reaction is complete, the sol is aged, and then template conditioning occurs. The template conditioning can include filtration, reflux, and rotoevaporation.

Next, template refinement occurs. This includes an optional drying step and calcination of the photocatalyst and additive particles. The result of the calcination step is a powder containing particles of the photocatalyst and particles of the additive. An aqueous slurry is then formed from the powder and is applied to the substrate by spraying, dip coating, or other application technique. Dispersants, pH modifiers, surfactants and the like may be used as mentioned previously to adjust the properties of the slurry to render it suitable for processing. After the solvent evaporates, the resulting coating includes the photocatalyst with intermixed particles of the additive.

Third, the photocatalyst coating, with the additives, can be in the form of multiple layers. For example, the photocatalyst layer can be deposited first, followed by a coating of the additive. The additive layer is an incomplete layer that does not cover the entire surface of photocatalyst. Instead, the resulting additive layer is in the form of islands of additive material on the surface of the photocatalyst. Formation of the islands or incomplete layer can be produced, for example, by vapor deposition, aerosol spray or solution precipitation techniques.

In some embodiments, the photocatalyst is titanium dioxide (titania) together with at least one other wide band gap semiconductor such as tin oxide, indium oxide, zinc oxide, iron oxide, neodymium oxide and cerium oxide. The photocatalyst may have enhanced resistance to deactivation by VSCCs by being formed of porous particles having a porous structure with pores of a diameter greater than about 6 nm and less than five populations of discrete pore size distributions. The porous particles are formed by crystallites that preferably are anatase titania, and have diameters of about 0.1 micron. The crystallites have diameters greater than about 2 nm.

In some embodiments, the additive particles can be in the form of dispersed, fine metal particles (e.g. Zr, Hf, Y, Al, etc.) that are selected for their potential to form oxides with relatively high reactivity towards, and therefore better scavenging ability of, the silicon-containing species.

In order to facilitate a reaction of the additive with volatile silicon-containing compounds to form a stable silicate, photocatalyst coating 22 may be temporarily or continually operated at an elevated temperature. The heating of photocatalyst coating 22 can be achieved by heater 28, for example, using resistive heating, microwave heating, infrared heating or a combination of these or similar heating methods.

Although the present invention has been described with reference to preferred embodiments, workers skilled in the art will recognize that changes may be made in form and detail without departing from the spirit and scope of the invention. 

1. A method of forming a UV photocatalyst, the method comprising: forming hydrolysis reactions to produce particles of an oxide capable of forming a stable silicate or solid solution with SiO₂ and particles of an oxide photocatalyst; filtering the particles produced by the hydrolysis reaction; refluxing the particles with a solvent having a lower surface tension than water; removing the solvent from the particles; calcining the particles; forming an aqueous slurry of the particles; and applying the aqueous slurry to a surface of a substrate.
 2. The method of claim 1 wherein the particles capable of forming a stable silicate or solid solution comprise at least one of a hafnium oxide, a zirconium oxide, a niobium oxide, an aluminum oxide, a magnesium oxide, a yttrium oxide, a tantalum oxide, a ytterbium oxide, a chromium oxide and a scandium oxide.
 3. The method of claim 1 wherein the oxide photocatalyst comprises titanium dioxide.
 4. The method of claim 3 wherein the oxide photocatalyst further comprises a wide band gap oxide semiconductor other than titanium dioxide.
 5. The method of claim 4 wherein the oxide photocatalyst further comprises at least one of tin oxide, indium oxide, zinc oxide, iron oxide, neodymium oxide and cerium oxide.
 6. The method of claim 1 wherein the step of forming hydrolysis reactions to produce particles of an oxide capable of forming a stable silicate or solid solution with SiO₂ and particles of an oxide photocatalyst comprises: adding a first precursor to a solution to produce particles of the oxide capable of forming a stable silicate or solid solution with SiO₂ with a first hydrolysis reaction; and adding a second precursor to the solution after the completion of the first hydrolysis reaction to produce particles of the oxide photocatalyst with a second hydrolysis reaction.
 7. A method of forming a photocatalytic device, the method comprising: forming particles of a sequestering agent with a sol-gel process; forming particles of a UV photocatalyst with the sol-gel process; calcining the particles; forming a slurry of the particles; and applying the slurry to a surface of a substrate to form a UV photocatalyst layer having sequestering agent particles dispersed therein.
 8. The method of claim 7 wherein the sequestering agent comprises at least one of a hafnium oxide, a zirconium oxide, a niobium oxide, an aluminum oxide, a magnesium oxide, a yttrium oxide, a tantalum oxide, a ytterbium oxide, a chromium oxide and a scandium oxide.
 9. The method of claim 7 wherein the UV photocatalyst comprises titanium dioxide.
 10. The method of claim 9 wherein the UV photocatalyst further comprises a wide band gap oxide semiconductor other than titanium dioxide.
 11. The method of claim 10 wherein the UV photocatalyst further comprises at least one of tin oxide, indium oxide, zinc oxide, iron oxide, neodymium oxide and cerium oxide.
 12. A method of forming a photocatalyst device, the method comprising: depositing a layer of a UV photocatalyst; depositing islands of a sequestering agent on a surface of the layer of the UV photocatalyst.
 13. The method of claim 12, wherein the sequestering agent comprises at least one of a hafnium oxide, a zirconium oxide, a niobium oxide, an aluminum oxide, a magnesium oxide, a yttrium oxide, a tantalum oxide, a ytterbium oxide, a chromium oxide and a scandium oxide.
 14. The method of claim 12, wherein the UV photocatalyst is a TiO₂-based photocatalyst.
 15. The method of claim 14, wherein the UV photocatalyst further comprises a wide band gap oxide semiconductor other than titanium dioxide.
 16. The method of claim 12, wherein the layer of the UV photocatalyst comprises porous photocatalyst particles having pores of a diameter equal to or greater than about 6 nm.
 17. The method of claim 16, wherein the porous photocatalyst particles have less than five populations of discrete pore size distributions.
 18. The method of claim 16, wherein the porous photocatalyst particles have about a 0.1 micron diameter.
 19. The method of claim 16, wherein the porous photocatalyst particles are formed by crystallites that are anatase particles.
 20. The method of claim 16, wherein the step of depositing islands of the sequestering agent comprises at least one method selected from the group consisting of: vapor deposition, aerosol spray and solution precipitation techniques. 